Valuable metals substance flow analysis in high-pressure acid leaching process of laterites
Substance flow analysis (SFA), an analytical tool, was applied to a high-pressure acid leaching (HPAL) process of laterites. The results show that although the HPAL process has become the mainstream process for the treatment of laterites, a large amount of solid waste discharge has caused great harm...
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Veröffentlicht in: | Journal of Central South University 2023-06, Vol.30 (6), p.1776-1786 |
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description | Substance flow analysis (SFA), an analytical tool, was applied to a high-pressure acid leaching (HPAL) process of laterites. The results show that although the HPAL process has become the mainstream process for the treatment of laterites, a large amount of solid waste discharge has caused great harm to the environment and restricted its large-scale development. The annual treatment capacity of laterites by HPAL process is 321×10
4
t, and 300×10
4
t of high-pressure leaching residue, 10×10
4
t of sulfate residue, 1.6×10
4
t of iron and aluminum residue, and 0.08×10
4
t of acid leaching residue are discharged every year. Nickel, cobalt, and manganese are used as the raw materials for the preparation of a precursor, and the masses finally flowing into the precursor preparation process are 2.70×10
4
t/a, 0.24×10
4
t/a, and 0.29×10
4
t/a, respectively, and the proportions are 77.14%, 75.00%, and 13.12%, respectively. Scandium finally flows into the scandium extraction process is 40.00 t/a, and the proportion is 37.70%. A total of 98.11% of iron and 99.86% of aluminum can be selectively removed by the high-pressure acid leaching. Some recommendations for improving emission control and resource recycling for the high-pressure acid leaching process of laterites are put forward in the conclusions of this study. |
doi_str_mv | 10.1007/s11771-023-5356-y |
format | Article |
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4
t, and 300×10
4
t of high-pressure leaching residue, 10×10
4
t of sulfate residue, 1.6×10
4
t of iron and aluminum residue, and 0.08×10
4
t of acid leaching residue are discharged every year. Nickel, cobalt, and manganese are used as the raw materials for the preparation of a precursor, and the masses finally flowing into the precursor preparation process are 2.70×10
4
t/a, 0.24×10
4
t/a, and 0.29×10
4
t/a, respectively, and the proportions are 77.14%, 75.00%, and 13.12%, respectively. Scandium finally flows into the scandium extraction process is 40.00 t/a, and the proportion is 37.70%. A total of 98.11% of iron and 99.86% of aluminum can be selectively removed by the high-pressure acid leaching. Some recommendations for improving emission control and resource recycling for the high-pressure acid leaching process of laterites are put forward in the conclusions of this study.</description><identifier>ISSN: 2095-2899</identifier><identifier>EISSN: 2227-5223</identifier><identifier>DOI: 10.1007/s11771-023-5356-y</identifier><language>eng</language><publisher>Changsha: Central South University</publisher><subject>Acid leaching ; Acids ; Aluminum ; Discharge ; Emissions control ; Engineering ; High pressure ; Iron ; Laterites ; Manganese ; Metallic Materials ; Nickel ; Precursors ; Pressure leaching ; Raw materials ; Residues ; Scandium ; Solid wastes</subject><ispartof>Journal of Central South University, 2023-06, Vol.30 (6), p.1776-1786</ispartof><rights>Central South University 2023</rights><rights>Central South University 2023.</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c316t-ce7df3ccfc9f5ac596dfe10d88ac9754e0e02781b09280e77482e723be26e1af3</citedby><cites>FETCH-LOGICAL-c316t-ce7df3ccfc9f5ac596dfe10d88ac9754e0e02781b09280e77482e723be26e1af3</cites><orcidid>0000-0003-0660-3024 ; 0000-0002-5960-9158</orcidid></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktopdf>$$Uhttps://link.springer.com/content/pdf/10.1007/s11771-023-5356-y$$EPDF$$P50$$Gspringer$$H</linktopdf><linktohtml>$$Uhttps://link.springer.com/10.1007/s11771-023-5356-y$$EHTML$$P50$$Gspringer$$H</linktohtml><link.rule.ids>315,781,785,27926,27927,41490,42559,51321</link.rule.ids></links><search><creatorcontrib>Tian, Qing-hua</creatorcontrib><creatorcontrib>Dong, Bo</creatorcontrib><creatorcontrib>Guo, Xue-yi</creatorcontrib><creatorcontrib>Wang, Qing-ao</creatorcontrib><creatorcontrib>Xu, Zhi-peng</creatorcontrib><creatorcontrib>Li, Dong</creatorcontrib><title>Valuable metals substance flow analysis in high-pressure acid leaching process of laterites</title><title>Journal of Central South University</title><addtitle>J. Cent. South Univ</addtitle><description>Substance flow analysis (SFA), an analytical tool, was applied to a high-pressure acid leaching (HPAL) process of laterites. The results show that although the HPAL process has become the mainstream process for the treatment of laterites, a large amount of solid waste discharge has caused great harm to the environment and restricted its large-scale development. The annual treatment capacity of laterites by HPAL process is 321×10
4
t, and 300×10
4
t of high-pressure leaching residue, 10×10
4
t of sulfate residue, 1.6×10
4
t of iron and aluminum residue, and 0.08×10
4
t of acid leaching residue are discharged every year. Nickel, cobalt, and manganese are used as the raw materials for the preparation of a precursor, and the masses finally flowing into the precursor preparation process are 2.70×10
4
t/a, 0.24×10
4
t/a, and 0.29×10
4
t/a, respectively, and the proportions are 77.14%, 75.00%, and 13.12%, respectively. Scandium finally flows into the scandium extraction process is 40.00 t/a, and the proportion is 37.70%. A total of 98.11% of iron and 99.86% of aluminum can be selectively removed by the high-pressure acid leaching. Some recommendations for improving emission control and resource recycling for the high-pressure acid leaching process of laterites are put forward in the conclusions of this study.</description><subject>Acid leaching</subject><subject>Acids</subject><subject>Aluminum</subject><subject>Discharge</subject><subject>Emissions control</subject><subject>Engineering</subject><subject>High pressure</subject><subject>Iron</subject><subject>Laterites</subject><subject>Manganese</subject><subject>Metallic Materials</subject><subject>Nickel</subject><subject>Precursors</subject><subject>Pressure leaching</subject><subject>Raw materials</subject><subject>Residues</subject><subject>Scandium</subject><subject>Solid wastes</subject><issn>2095-2899</issn><issn>2227-5223</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2023</creationdate><recordtype>article</recordtype><recordid>eNp1kE9LxDAUxIsouOh-AG8Bz9HkZZs0R1n8Bwte1IuHkKYvu5FuuyYt0m9vlgqePL2BNzMMv6K44uyGM6ZuE-dKccpA0FKUkk4nxQIAFC0BxGnWTJcUKq3Pi2VKoWaCgxRSy0Xx8W7b0dYtkj0Otk0kjXUabOeQ-Lb_Jraz7ZRCIqEju7Dd0UPElMaIxLrQkBat24VuSw6xd_lBek9aO2AMA6bL4sznSlz-3ovi7eH-df1ENy-Pz-u7DXWCy4E6VI0XznmnfWldqWXjkbOmqqzTqlwhQwaq4jXTUDFUalUBKhA1gkRuvbgorufePOJrxDSYz36MeXgyUK24VlyCzi4-u1zsU4rozSGGvY2T4cwcMZoZo8kYzRGjmXIG5kzK3m6L8a_5_9APlfV3Nw</recordid><startdate>20230601</startdate><enddate>20230601</enddate><creator>Tian, Qing-hua</creator><creator>Dong, Bo</creator><creator>Guo, Xue-yi</creator><creator>Wang, Qing-ao</creator><creator>Xu, Zhi-peng</creator><creator>Li, Dong</creator><general>Central South University</general><general>Springer Nature B.V</general><scope>AAYXX</scope><scope>CITATION</scope><orcidid>https://orcid.org/0000-0003-0660-3024</orcidid><orcidid>https://orcid.org/0000-0002-5960-9158</orcidid></search><sort><creationdate>20230601</creationdate><title>Valuable metals substance flow analysis in high-pressure acid leaching process of laterites</title><author>Tian, Qing-hua ; Dong, Bo ; Guo, Xue-yi ; Wang, Qing-ao ; Xu, Zhi-peng ; Li, Dong</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c316t-ce7df3ccfc9f5ac596dfe10d88ac9754e0e02781b09280e77482e723be26e1af3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2023</creationdate><topic>Acid leaching</topic><topic>Acids</topic><topic>Aluminum</topic><topic>Discharge</topic><topic>Emissions control</topic><topic>Engineering</topic><topic>High pressure</topic><topic>Iron</topic><topic>Laterites</topic><topic>Manganese</topic><topic>Metallic Materials</topic><topic>Nickel</topic><topic>Precursors</topic><topic>Pressure leaching</topic><topic>Raw materials</topic><topic>Residues</topic><topic>Scandium</topic><topic>Solid wastes</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Tian, Qing-hua</creatorcontrib><creatorcontrib>Dong, Bo</creatorcontrib><creatorcontrib>Guo, Xue-yi</creatorcontrib><creatorcontrib>Wang, Qing-ao</creatorcontrib><creatorcontrib>Xu, Zhi-peng</creatorcontrib><creatorcontrib>Li, Dong</creatorcontrib><collection>CrossRef</collection><jtitle>Journal of Central South University</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Tian, Qing-hua</au><au>Dong, Bo</au><au>Guo, Xue-yi</au><au>Wang, Qing-ao</au><au>Xu, Zhi-peng</au><au>Li, Dong</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Valuable metals substance flow analysis in high-pressure acid leaching process of laterites</atitle><jtitle>Journal of Central South University</jtitle><stitle>J. Cent. South Univ</stitle><date>2023-06-01</date><risdate>2023</risdate><volume>30</volume><issue>6</issue><spage>1776</spage><epage>1786</epage><pages>1776-1786</pages><issn>2095-2899</issn><eissn>2227-5223</eissn><abstract>Substance flow analysis (SFA), an analytical tool, was applied to a high-pressure acid leaching (HPAL) process of laterites. The results show that although the HPAL process has become the mainstream process for the treatment of laterites, a large amount of solid waste discharge has caused great harm to the environment and restricted its large-scale development. The annual treatment capacity of laterites by HPAL process is 321×10
4
t, and 300×10
4
t of high-pressure leaching residue, 10×10
4
t of sulfate residue, 1.6×10
4
t of iron and aluminum residue, and 0.08×10
4
t of acid leaching residue are discharged every year. Nickel, cobalt, and manganese are used as the raw materials for the preparation of a precursor, and the masses finally flowing into the precursor preparation process are 2.70×10
4
t/a, 0.24×10
4
t/a, and 0.29×10
4
t/a, respectively, and the proportions are 77.14%, 75.00%, and 13.12%, respectively. Scandium finally flows into the scandium extraction process is 40.00 t/a, and the proportion is 37.70%. A total of 98.11% of iron and 99.86% of aluminum can be selectively removed by the high-pressure acid leaching. Some recommendations for improving emission control and resource recycling for the high-pressure acid leaching process of laterites are put forward in the conclusions of this study.</abstract><cop>Changsha</cop><pub>Central South University</pub><doi>10.1007/s11771-023-5356-y</doi><tpages>11</tpages><orcidid>https://orcid.org/0000-0003-0660-3024</orcidid><orcidid>https://orcid.org/0000-0002-5960-9158</orcidid></addata></record> |
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subjects | Acid leaching Acids Aluminum Discharge Emissions control Engineering High pressure Iron Laterites Manganese Metallic Materials Nickel Precursors Pressure leaching Raw materials Residues Scandium Solid wastes |
title | Valuable metals substance flow analysis in high-pressure acid leaching process of laterites |
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